CN213576815U - Oil field low pressure flash distillation gas pipeline defeated hydrops control system that stops - Google Patents
Oil field low pressure flash distillation gas pipeline defeated hydrops control system that stops Download PDFInfo
- Publication number
- CN213576815U CN213576815U CN202022454737.4U CN202022454737U CN213576815U CN 213576815 U CN213576815 U CN 213576815U CN 202022454737 U CN202022454737 U CN 202022454737U CN 213576815 U CN213576815 U CN 213576815U
- Authority
- CN
- China
- Prior art keywords
- pipeline
- gas
- flash
- flash evaporation
- valve
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Landscapes
- Pipeline Systems (AREA)
Abstract
The utility model discloses a control system for the liquid accumulation in the oil field by the low-pressure flash evaporation gas pipeline, which comprises a high-temperature gas reverse purging system, an upper auxiliary pressure relief system, a flash evaporation gas treatment plant rapid relief system and a matched detection system; the high-temperature gas reverse purging system is used for providing high-temperature gas for the flash evaporation gas trunk line which stops conveying, gasifying accumulated liquid in the pipeline and replacing media in the pipeline; the upstream auxiliary pressure relief system is used for flash evaporation gas relief in the reverse purging process of the flash evaporation gas pipeline after the stop of the transportation; the rapid discharge system of the flash evaporation gas treatment plant is used for rapidly discharging a medium in a flash evaporation gas pipeline after the transportation is stopped or directly discharging the flash evaporation gas pipeline when the treatment plant does not supply reverse purge gas; the associated sensing system is used for sensing temperature, pressure and flow at desired locations in the system to provide operational input signals and input parameters. The utility model discloses can carry out effective control to flash distillation gas pipeline hydrops in essence, reduce the influence to the restart process.
Description
Technical Field
The utility model belongs to the technical field of oil field flash distillation gas pipeline transport, in particular to oil field low pressure flash distillation gas pipeline defeated hydrops control system that stops.
Background
In the crude oil treatment process of an oil field central treatment plant, in order to ensure the quality of oil products, the saturated vapor pressure of the oil products needs to be controlled, more flash evaporation gas is separated from the oil products, and the oil products are generally directly discharged. Along with the continuous deepening of the requirements on energy conservation and emission reduction and reasonable resource utilization, the recycling of flash steam is advocated. The flash steam is a better oil field fuel gas and can be collected and treated in a centralized way to be supplied to various public facilities in the oil field. The flash gas contains more C1-C5 components, the specific composition of the flash gas is influenced by the crude oil stabilizing process, and the dew point temperature at low pressure is generally higher. In the transformation or upgrading of a large-scale oil field, the flash steam of each central processing plant and degassing station in the oil field is generally considered to be conveyed to a newly-built central flash steam processing plant through a plurality of gathering and conveying pipelines, and a system mode that a plurality of paths of flash steam collecting (recycling) pipelines are connected to the central flash steam processing plant is formed so as to further carry out flash steam processing and utilization.
The oil field flash gas pipeline is limited by an upstream oil product stabilizing process, the operation pressure is generally lower, but the gas source temperature is generally higher. For flash steam with relatively high C3-C5 content, condensate liquid in a pipeline is more easily generated due to the influence of the environment in the conveying process, and especially in winter working conditions, more accumulated liquid is often existed in a tail-end pipeline. If the pigging operation is performed at this time, a large slug load may be caused. In order to control the size of the plug flow catcher at the downstream section, the operation side generally considers that the pipeline is cleaned in summer with higher ambient temperature, and the accumulated liquid in the pipeline is relatively less due to higher ambient temperature.
In a flash steam pipeline system, partial pipeline overhauling stop is a planned operation condition. For oil field flash distillation gas pipeline, if carry out the pipeline under the lower condition of ambient temperature and stop defeated, medium temperature will be unanimous with ambient environment fast because of the heat exchange in the pipeline, and most heavy hydrocarbon will take place the liquefaction in the medium this moment, leads to the further increase of hydrops in the pipeline, promotes the receiving load of downstream section plug flow catcher, influences the pipeline restart on next step. Although it can be solved by prolonging the pipeline re-production operation time, it directly affects the re-production speed, causing some economic loss. However, the prior art has not dealt with specific measures and solutions in this regard.
Therefore, in order to reduce the risk of liquid accumulation after the pipeline of the low-pressure flash evaporation gas in the oil field stops conveying, related control scheme research is carried out on the basis of the characteristics of the recovery pipeline system of the flash evaporation gas in the oil field and the gas quality characteristics of the low-pressure flash evaporation gas pipeline by taking safety and economy as targets, and liquid accumulation management after the pipeline of the low-pressure flash evaporation gas stops conveying is reasonably carried out.
SUMMERY OF THE UTILITY MODEL
The invention of the utility model aims to: aiming at the problems, the oil field low-pressure flash evaporation gas pipeline transportation-stop accumulated liquid control system can further improve the operation technology of the low-pressure oil field flash evaporation gas pipeline.
The main technical idea of the utility model is based on the characteristic that the dew point of the stored gas in the low-pressure flash evaporation gas pipeline is higher, the influence of the accumulated liquid on the restarting after the stop of the transportation of the flash evaporation gas collecting pipeline is comprehensively considered, the process of the oil field flash evaporation gas collecting and treating system is fully combined, properly perfecting a flash evaporation gas treatment system, arranging a high-temperature gas reverse purging system, an upstream auxiliary pressure relief system, a flash evaporation gas treatment plant rapid relief system, a matched control system and the like aiming at a pipeline with a large liquid accumulation risk (the maximum liquid accumulation amount of the pipeline during the stop of transportation exceeds the load of a treatment plant slug flow catcher), promoting the pressure reduction, gasification and relief of media in the pipeline after the stop of transportation, and further, high-temperature gas is reversely blown and swept, so that distribution adjustment of residual effusion and secondary heating gasification and discharge of the residual effusion are realized, the restarting operation difficulty is reduced to the maximum extent, and the effusion control effect under the condition that a high-effusion flash evaporation gas pipeline of the oil field flash evaporation gas recovery system stops conveying is ensured.
The utility model adopts the technical proposal that:
the utility model provides an oil field low pressure flash distillation gas pipeline defeated hydrops control system that stops which characterized in that: the system comprises a high-temperature gas reverse purging system, an upstream auxiliary pressure relief system, a flash evaporation gas treatment plant rapid relief system and a matched detection system;
the high-temperature gas reverse purging system is connected with the flash evaporation gas main line which stops conveying, and is used for providing high-temperature gas for the flash evaporation gas main line which stops conveying, gasifying accumulated liquid in the pipeline and replacing media in the pipeline;
the upstream auxiliary pressure relief system is arranged in an upstream oil field treatment or degassing station plant and is used for flash evaporation gas relief in the process of reverse purging of a flash evaporation gas pipeline after the transportation is stopped;
the rapid discharge system of the flash evaporation gas treatment plant is arranged at the tail end of the flash evaporation gas collecting and conveying pipeline, is connected with the flash evaporation gas collecting and conveying pipeline with liquid accumulation risk and a discharge system of the flash evaporation gas treatment plant, and is used for rapidly discharging media in the flash evaporation gas pipeline after the transportation is stopped or directly discharging the flash evaporation gas pipeline when reverse purge gas is not supplied to the treatment plant;
the associated sensing system is used for sensing temperature, pressure and flow at desired locations in the system to provide operational input signals and input parameters.
The utility model discloses an oil field low pressure flash distillation gas pipeline defeated hydrops control system that stops, its high temperature gas reverse purge system includes that one-level compressor exports the lateral conduit, one-level air cooler exports the lateral conduit and the mixed pipeline of reverse purge gas;
the outlet branch pipeline of the primary compressor is connected with an outlet of a primary pressurizing unit of a flash evaporation gas treatment plant and is used for providing a high-temperature raw material gas after primary pressurization as a high-temperature gas source for reversely purging by a single pipeline;
the outlet branch pipeline of the primary air cooler is connected with an outlet of the air cooler of a flash evaporation gas treatment plant, and is used for extracting air-cooled raw material gas and mixing the air-cooled raw material gas with high-temperature raw material gas from the outlet branch pipeline of the primary compressor;
and the reverse purge gas mixing pipeline is connected with the branch pipeline at the outlet of the primary compressor and the branch pipeline at the outlet of the primary air cooler and is used for conveying the mixed medium to the tail end of the flash evaporation gas gathering and conveying pipeline.
The utility model discloses an oil field low pressure flash distillation gas pipeline defeated hydrops control system that stops, it is provided with reverse purge gas pipeline first shut-off valve and reverse purge gas pipeline first governing valve on the branch pipeline of first order compressor export, reverse purge gas pipeline first governing valve is installed in the downstream of reverse purge gas pipeline first shut-off valve;
a second cut-off valve of the reverse purge gas pipeline and a second regulating valve of the reverse purge gas pipeline are arranged on the branch pipeline at the outlet of the primary air cooler, and the second regulating valve of the reverse purge gas pipeline is arranged at the downstream of the second cut-off valve of the reverse purge gas pipeline;
and a third cutoff valve of the reverse purge gas pipeline is arranged at the tail end of the reverse purge gas mixing pipeline, and is opened when the reverse purge gas system is started, wherein the opening sequence of the third cutoff valve is prior to that of the first cutoff valve of the reverse purge gas pipeline and that of the second cutoff valve of the reverse purge gas pipeline.
Oil field low pressure flash distillation gas pipeline defeated hydrops control system that stops, its upper reaches auxiliary pressure discharge system includes the upper reaches pipeline of releasing and sets up upper reaches pipeline of releasing on the pipeline of releasing of upper reaches interception valve and upper reaches governing valve of releasing, upper reaches pipeline of releasing interception is used for providing the unloading passageway when medium releases to the oil field processing factory unloading system of upper reaches in the flash distillation gas pipeline, the governing valve of releasing of upper reaches is used for controlling the volume of releasing when releasing, the pipeline connection oil field processing factory of releasing of upper reaches has built the unloading system.
Oil field low pressure flash distillation gas pipeline defeated hydrops control system that stops, its flash distillation gas treatment factory fast bleed system includes flash distillation gas pipeline low reaches discharge conduit and sets up low reaches on flash distillation gas pipeline low reaches discharge conduit and release the intercept valve and the low reaches governing valve of releasing, low reaches are released and are cut the intercept valve and open earlier after flash distillation gas pipeline fails, release intraductal accumulated gas, low reaches are released the governing valve and are released the intercept valve and open simultaneously with low reaches, flash distillation gas pipeline low reaches discharge conduit connects the unloading system of flash distillation gas treatment factory.
The utility model discloses an oil field low pressure flash distillation gas pipeline loses defeated hydrops control system, its supporting detecting system includes first pressure transmitter, first temperature transmitter, first flow transmitter, second pressure transmitter, second temperature transmitter and second flow transmitter;
the first pressure transmitter, the first temperature transmitter and the first flow transmitter are arranged at the beginning end of the reverse purge gas mixing pipeline and are respectively used for detecting the pressure, the temperature and the flow of the mixed gas;
the second pressure transmitter is arranged at the head end of the rapid release system of the flash evaporation gas treatment plant and is used for detecting the pressure of the flash evaporation gas trunk line in real time;
the second temperature transmitter and the second flow transmitter are respectively installed on a discharge pipeline of the upstream auxiliary pressure discharge system and are respectively used for detecting the local medium temperature of the flash evaporation gas pipeline and the accumulated discharge medium in the flash evaporation gas reverse purging process.
Compared with the prior art, the utility model has the positive effects that: the method is characterized in that based on the characteristic that the dew point of stored gas in a low-pressure flash gas pipeline is high and the distribution rule of accumulated liquid in the flash gas pipeline, the influence of accumulated liquid on restarting after the stop of the delivery of the flash gas collecting pipeline is comprehensively considered, the process is fully based on the process of the oil field flash gas collecting and processing system, the flash gas processing system is properly perfected, a high-temperature gas reverse purging system, an upstream auxiliary pressure relief system, a flash gas processing plant rapid relief system, a matched control system and the like are arranged for the pipeline with large accumulated liquid risk, the accumulated liquid in the flash gas pipeline is effectively controlled essentially, and the influence on the restarting process is reduced.
The concrete expression is as follows:
(1) science of setup
The utility model discloses a to the abundant understanding of medium characteristics in the flash distillation gas pipeline, the pipeline that has higher hydrops risk after stopping defeated among the screening multichannel flash distillation gas pipeline carries out the pertinence control, considers the overall thought that adopts to stop defeated back and release fast, avoids the medium to appear a large amount of liquid phases and increase total hydrops volume in the pipeline under ambient temperature's influence. Preferably, a pressurization system arranged in a flash gas treatment plant is adopted to provide a high-temperature medium, a target flash gas pipeline is reversely swept, the flash gas which is stopped to be transported in the pipeline is replaced by the pressurization gas with less liquid content, the liquid accumulation risk is further reduced, and the temperature of the medium in the pipeline and the existing liquid accumulation is improved by injecting the pressurized gas into the flash gas pipeline with the help of the characteristic that the temperature of the gas after primary compression is higher, so that part of the liquid accumulation is gasified, and the liquid accumulation in the original pipeline is reduced. Meanwhile, the working condition that no pressurized gas is available when the treatment plant is stopped is considered, the rapid pressure relief system is directly arranged to release the flash evaporation gas in the pipeline, and a large amount of liquid separated out from the flash evaporation gas in the pipeline after long-term stop is avoided.
(2) Good economical efficiency
The utility model discloses there are not newly-built large-scale device and equipment, only set up the high-temperature gas reverse purging system who need not extra energy supply and provide blowback air supply and unloading system connecting tube way, can effectively reduce the pipeline hydrops, from the permanent slug flow catcher size that has reduced the setting in essence, better economic nature has.
(3) Promote the technical progress
The utility model discloses fully consider the hydrops law of flash distillation gas gathering and transportation pipeline, innovatively according to stopping the characteristics that defeated back hydrops volume increase is higher than conventional gathering and transportation pipeline, for reducing the follow-up restart process degree of difficulty, through multiple scheme comparison, take the counterblow to sweep and the measure of releasing fast, realize the initiative of medium in the pipeline and arrange outward, the hydrops increase of volume after effective control stops defeated in the pipeline, novelty and feasibility have been had, the mobile guarantee technical research direction of flash distillation gas gathering and transportation pipeline has been expanded, the technological development and the progress of this type of pipeline have been promoted.
Drawings
The invention will be described by way of example only and with reference to the accompanying drawings, in which
Fig. 1 is a schematic view of the present invention.
The labels in the figure are: 1 is a buried flash gas collecting and conveying trunk line, 2 is an upstream outbound pipeline, 3 is a downstream inbound pipeline, 4 is an upstream outbound cut-off valve, 5 is a downstream inbound cut-off valve, 6 is a primary pressurizing unit, 7 is an air cooler, 8 is an interstage separator, 9 is a gas-liquid separator, 11 is a primary compressor outlet branch pipeline, 12 is a primary air cooler outlet branch pipeline, 13 is a reverse scavenging gas mixing pipeline, 14 is a reverse scavenging gas pipeline first cut-off valve, 15 is a reverse scavenging gas pipeline second cut-off valve, 16 is a reverse scavenging gas pipeline first regulating valve, 17 is a reverse scavenging gas pipeline second regulating valve, 18 is a reverse scavenging gas pipeline third cut-off valve, 21 is an upstream discharge pipeline cut-off valve, 22 is an upstream discharge regulating valve, 23 is an upstream discharge pipeline, 31 is a downstream discharge cut-off valve, 32 is a downstream discharge regulating valve, 33 is a flash gas pipeline downstream discharge pipeline, 41 is a first pressure transmitter, 42 is a first temperature transmitter, 43 is a first flow transmitter, 44 is a second pressure transmitter, 45 is a second temperature transmitter, and 46 is a second flow transmitter.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all, embodiments of the present invention. The components of embodiments of the present invention, as generally described and illustrated in the figures herein, may be arranged and designed in a wide variety of different configurations.
Thus, the following detailed description of the embodiments of the present invention, presented in the accompanying drawings, is not intended to limit the scope of the invention, as claimed, but is merely representative of selected embodiments of the invention. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts belong to the protection scope of the present invention.
It should be noted that, in the present invention, the embodiments and features of the embodiments may be combined with each other without conflict.
It should be noted that: like reference numbers and letters refer to like items in the following figures, and thus, once an item is defined in one figure, it need not be further defined and explained in subsequent figures.
In the description of the embodiments of the present invention, it should be noted that the indication of the position or the positional relationship is based on the position or the positional relationship shown in the drawings, or the position or the positional relationship that the utility model is usually placed when using, or the position or the positional relationship that the skilled person conventionally understands, or the position or the positional relationship that the utility model is usually placed when using, and is only for the convenience of describing the present invention and simplifying the description, but does not indicate or suggest that the indicated device or element must have a specific position, be constructed and operated in a specific position, and thus, cannot be understood as limiting the present invention. Furthermore, the terms "first" and "second" are used merely to distinguish one description from another, and are not to be construed as indicating or implying relative importance.
In the description of the embodiments of the present invention, it should be further noted that unless otherwise explicitly stated or limited, the terms "disposed" and "connected" should be interpreted broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; may be directly connected or indirectly connected through an intermediate. The specific meaning of the above terms in the present invention can be understood in specific cases for a person of ordinary skill in the art; the drawings in the embodiments are provided to clearly and completely describe the technical solutions in the embodiments of the present invention, and it is obvious that the described embodiments are some, not all embodiments of the present invention. The components of embodiments of the present invention, as generally described and illustrated in the figures herein, may be arranged and designed in a wide variety of different configurations.
As shown in fig. 1, a pipeline system for conveying low-pressure flash evaporation gas in an oil field comprises a buried flash evaporation gas conveying trunk line 1, an upstream outbound pipeline 2, a downstream inbound pipeline 3, an upstream outbound block valve 4 and a downstream inbound block valve 5, and is used for conveying flash evaporation gas recovered by an oil field central treatment plant to a flash evaporation gas downstream treatment plant in a normal production process.
Specifically, the flash evaporation gas buried gathering and transportation trunk line 1, the upstream outbound pipeline 2 and the downstream inbound pipeline 3 are the same in outer diameter, so that the pipe cleaning function can be met, and the material is determined according to the design temperature, the design pressure, the medium composition and the like; the upstream outbound cut-off valve 4 and the downstream inbound cut-off valve 5 are both electric ball valves, are normally open, and are closed when the planned delivery is stopped.
The control system comprises a high-temperature gas reverse purging system, an upstream auxiliary pressure relief system, a flash gas treatment plant rapid relief system and a matched detection system.
The high-temperature gas reverse purging system is connected with the flash evaporation gas trunk line which stops conveying, and is used for providing high-temperature gas for the flash evaporation gas trunk line which stops conveying, gasifying accumulated liquid in the pipeline and replacing media in the pipeline; specifically, the high-temperature gas reverse purging system comprises a primary compressor outlet branch pipeline 11, a primary air cooler outlet branch pipeline 12 and a reverse purging gas mixing pipeline 13, wherein the primary compressor outlet branch pipeline 11 is connected to an outlet of a primary pressurizing unit 6 of a flash evaporation gas treatment plant and is used for providing a primary pressurized high-temperature raw gas as a high-temperature gas source for reverse purging of a single stop pipeline, in the embodiment, the primary compressor outlet branch pipeline is connected out of the compressor outlet pipeline, is made of the same material as the compressor outlet pipeline, and has a pipe diameter which is determined by the fact that the flow rate of the reverse purging gas in the pipeline is not more than 20m/s and is used for providing the high-temperature (about 150 ℃) reverse purging gas; the primary air cooler outlet branch pipeline 12 is connected to an outlet of an air cooler 7 of a flash gas treatment plant and used for extracting air-cooled raw material gas, mixing the air-cooled raw material gas with high-temperature raw material gas from a primary compressor outlet branch pipeline 11 and adjusting the temperature of the mixture to meet the requirement of the highest temperature of a flash gas inlet; the reverse blowing gas mixing pipeline 13 is connected with a branch pipeline 11 at the outlet of the primary compressor and a branch pipeline 12 at the outlet of the primary air cooler, the tail end of the reverse blowing gas mixing pipeline is connected with a flash gas main pipeline (inlet of a treatment plant) and used for conveying mixed media to the tail end of a flash gas collecting and conveying pipeline and providing high-temperature gas after pressure regulation for the flash gas main pipeline which stops conveying, and the material of the reverse blowing gas mixing pipeline is consistent with that of the downstream station-entering pipeline 3.
Specifically, a reverse purge gas pipeline first cut-off valve 14 and a reverse purge gas pipeline first regulating valve 16 are arranged on the primary compressor outlet branch pipeline 11, the reverse purge gas pipeline first cut-off valve 14 is a manual ball valve, is normally closed, and is opened when the reverse purge system is started, the reverse purge gas pipeline first regulating valve 16 is an electric regulating valve, the opening degree is regulated under the coordination indication of a downstream temperature transmitter and a flow transmitter, the regulation of the opening degree should also be coordinated with a reverse purge gas pipeline second regulating valve 17, and the reverse purge gas pipeline first regulating valve 16 is installed at the downstream of the reverse purge gas pipeline first cut-off valve 14; a second cut-off valve 15 of a reverse purge gas pipeline and a second regulating valve 17 of the reverse purge gas pipeline are arranged on the outlet branch pipeline 12 of the primary air cooler, the second cut-off valve 15 of the reverse purge gas pipeline is a manual ball valve, is normally closed and is opened when the reverse purge system is started, the second regulating valve 17 of the reverse purge gas pipeline is an electric regulating valve, the opening degree of the second regulating valve is regulated under the coordination indication of a downstream temperature transmitter and a flow transmitter, the regulation of the opening degree of the second regulating valve also needs to be coordinated with the first regulating valve 16 of the reverse purge gas pipeline, and the second regulating valve 17 of the reverse purge gas pipeline is arranged at the downstream of the second cut-off valve 15 of the reverse purge gas pipeline; and a third reverse purge gas pipeline cutoff valve 18 is arranged at the tail end of the reverse purge gas mixing pipeline 13, the third reverse purge gas pipeline cutoff valve 18 is a manual ball valve, is normally closed, and is opened when the reverse purge system is started, and the opening sequence of the third reverse purge gas pipeline cutoff valve 18 is prior to that of the first reverse purge gas pipeline cutoff valve 14 and the second reverse purge gas pipeline cutoff valve 15.
The system comprises an upstream auxiliary pressure relief system, a downstream auxiliary pressure relief system and a downstream auxiliary pressure relief system, wherein the upstream auxiliary pressure relief system is arranged in an upstream oil field treatment or degassing station plant, and is mainly used for flash gas relief of the upstream oil field or degassing station in emergency by relying on an established relief system of the upstream oil field treatment plant or degassing station, and is used for flash gas relief in a reverse purging process of a flash gas pipeline after the pipeline is stopped; specifically, the upstream auxiliary pressure relief system comprises an upstream relief pipeline 23, and an upstream relief pipeline cut-off valve 21 and an upstream relief regulating valve 22 which are arranged on the upstream relief pipeline 23, wherein the upstream relief pipeline cut-off valve 21 is a manual ball valve and is normally closed, and is used for providing a venting channel when the medium in the flash gas pipeline is released to a venting system of an upstream oil field treatment plant; the upper stream relief regulating valve 22 is a manual regulating valve and is normally closed, and is used for controlling the relief amount during relief, the upper stream relief pipeline 23 is connected with an established relief system of an oil field treatment plant and is made of normal-temperature carbon steel.
The rapid discharge system of the flash evaporation gas treatment plant is arranged at the tail end of the flash evaporation gas collecting and conveying pipeline, is connected with the flash evaporation gas collecting and conveying pipeline with liquid accumulation risk and a discharge system of the flash evaporation gas treatment plant, and is used for rapidly discharging media in the flash evaporation gas pipeline after the transportation is stopped or directly discharging the flash evaporation gas pipeline when the treatment plant has no reverse purge gas supply, so that the phenomenon that a large amount of liquid phase in the pipeline is separated out after the transportation is stopped for too long time is avoided; specifically, the rapid discharge system of the flash gas treatment plant comprises a flash gas pipeline downstream discharge pipeline 33, and a downstream discharge cut-off valve 31 and a downstream discharge regulating valve 32 which are arranged on the flash gas pipeline downstream discharge pipeline 33, wherein the downstream discharge cut-off valve 31 is a manual ball valve and is normally closed, and is opened in advance after the flash gas pipeline stops delivering, so that gas is accumulated in the discharge pipeline; the downstream discharge regulating valve 32 and the downstream discharge cutoff valve 31 are opened simultaneously, and the flash evaporation gas pipeline downstream discharge pipeline 33 is connected with a venting system of a flash evaporation gas treatment plant and is made of normal-temperature carbon steel.
The matched detection system is used for detecting the temperature, the pressure and the flow of a required position in the system so as to provide an operation input signal and an input parameter; specifically, the matching detection system includes a first pressure transmitter 41, a first temperature transmitter 42, a first flow transmitter 43, a second pressure transmitter 44, a second temperature transmitter 45 and a second flow transmitter 4, the first pressure transmitter 41, the first temperature transmitter 42 and the first flow transmitter 43 are installed at the start end of the reverse purge gas mixing pipeline 13 and are respectively used for detecting the pressure, the temperature and the flow of the mixed gas so as to adjust the opening of the regulating valve on the two reverse purge gas pipelines and the proportion of the two reverse purge gases, the second pressure transmitter 44 is installed at the head end of the rapid discharge system of the flash gas treatment plant and is used for detecting the pressure of a flash gas trunk line in real time, and the second temperature transmitter 45 and the second flow transmitter 46 are respectively installed on the discharge pipeline of the upstream auxiliary pressure discharge system and are respectively used for detecting the local medium temperature of the flash gas pipeline and the accumulated discharge medium in the flash gas reverse purge process And (6) detecting.
Therefore, the system for controlling the liquid accumulation during the stop of the delivery of the low-pressure flash evaporation gas pipeline system in the oil field is formed, and the safety guarantee can be provided for the subsequent operation after the stop of the delivery of the flash evaporation gas in the oil field.
The utility model discloses a theory of operation does:
(1) during the decompression flash evaporation stabilization process, crude oil produced in the oil field generates more low-pressure flash evaporation gas which contains more gaseous hydrocarbon components. The flash gas produced by a plurality of crude oil processing plants in the oil field is collected to the flash gas processing plant for centralized collection and processing. The flash evaporation gas is inevitably subjected to temperature reduction in the conveying process, so that partial hydrocarbons are liquefied and separated out and form accumulated liquid, and the principle of the accumulated liquid is obviously different from the accumulated liquid rule of a gathering and conveying pipeline of a conventional water and gas production field. The accumulated liquid in the flash evaporation gas pipeline has a regasification condition, so that reasonable measures can be taken for utilization, and the volume requirement on the plug flow catcher in the downstream section is reduced.
(2) In normal operation, the technical characteristics of the flash evaporation gas pipeline are basically consistent with those of the conventional gas field gathering and transportation pipeline, and flash evaporation gas generated at the upstream is conveyed after entering the pipeline and enters a flash evaporation gas treatment plant and enters a subsequent treatment device after passing through a slug flow catcher (or a separator); meanwhile, a multistage pressurization system is arranged in a flash evaporation gas treatment plant and used for centralized treatment after pressurization of flash evaporation gas, and the treatment efficiency is improved.
(3) And for the treatment plant with a plurality of flash steam supplies, selecting a pipeline with the accumulated liquid amount exceeding the allowable receiving capacity of the slug catcher of the flash steam treatment plant after the pipeline of the flash steam stops delivering to perform accumulated liquid stop delivery control through simulation analysis. Furthermore, before the flash evaporation gas pipeline is stopped, partial liquid accumulation occurs in the pipeline, mainly in the flowing process of the flash evaporation gas entering the pipeline, the temperature is gradually reduced due to heat exchange with the environment, the dew point of partial components is reached, and the liquid accumulation in the pipeline is formed; the liquid loading in the second half of the pipeline is obviously more than that in the first half of the pipeline.
(4) The pipeline stops initial stage behind the defeated, because remaining flash distillation gas has relatively higher temperature in the pipeline, and has certain pressure, is the good opportunity of releasing to low pressure flash distillation gas this moment, starts the system of releasing fast of flash distillation gas processing factory, carries out the pressure release with the medium in the flash distillation gas pipeline rapidly, avoids heavy component in the remaining flash distillation gas on the one hand because the further emergence liquefaction of losing time overlength, and on the other hand is through stepping down, can gasify a small amount of condensate again, discharge system in the lump. Because the flash evaporation gas pipeline gas is the flash evaporation gas of the oil field, and the pressure is lower, compared with a newly-built large-scale slug flow catcher, the economic efficiency is better by adopting an active discharge mode.
(5) Further, there is a condensate within the pipe that cannot be vaporized due in part to temperature effects. At the moment, the reverse purging system is started, other air inflow conditions of the flash evaporation gas treatment plant are utilized, high-temperature gas separated by the inlet gas-liquid separator 9 is led out from the back of the primary compressor, gas separated by the inlet and the primary pressurization is led out from the outlet of the primary air cooler, two paths of gas are blended, the reverse purging air inflow temperature condition meeting the design temperature of the flash evaporation gas highest pipeline is achieved, on one hand, accumulated liquid in the flash evaporation gas pipeline is reversely carried, on the other hand, the accumulated liquid is heated, and the effects of gasifying the rest accumulated liquid and adjusting the distribution of the accumulated liquid are achieved. At the same time, the vent system of the upstream oilfield treatment plant is turned on to provide a vent path for the reverse purge gas.
(6) After the operation is carried out according to the design direction purging time, the total amount of accumulated liquid in the flash evaporation gas pipeline is greatly reduced, the accumulated liquid distribution is not accumulated in the rear half section of the pipeline any more, the dew point of residual gas is lower, and an effective control effect is provided for the problem of accumulated liquid in the pipeline in the subsequent restarting process.
Additionally, the utility model discloses still formed an oil field low pressure flash distillation gas piping system and stopped defeated hydrops control method, specifically do:
the method comprises the following steps: in a multi-channel flash steam collecting pipeline which is transported to a flash steam treatment plant in an oil field, selecting a pipeline as a protection object, wherein the total volume and liquid of the pipeline after transportation stop may exceed the design load of a plug flow catcher in a downstream section through simulation analysis and calculation, and setting a liquid accumulation control system; the effusion control system comprises a high-temperature gas reverse purging system, an upstream auxiliary pressure relief system, a flash evaporation gas treatment plant rapid relief system and a matched detection system.
Step two: when the system normally operates, the high-temperature gas reverse purging system, the upstream auxiliary pressure relief system and the flash gas treatment plant rapid relief system are kept in a closed state; specifically, the inlet block valve (two-way) of the reverse purging pipeline is kept closed, the outlet block valve of the reverse purging pipeline is kept closed, the inlet block valve of the upstream auxiliary pressure relief system is kept closed, and the block valve of the rapid relief system of the flash vapor treatment plant is kept closed.
Step three: when the planned transportation stop of a target protection main line but normal operation of a flash evaporation gas treatment plant and other plant inlet pipelines, firstly starting a rapid release system of the flash evaporation gas treatment plant, rapidly introducing the existing stored gas into a low-pressure emptying system of the treatment plant, and finally finishing the release of the transportation stop flash evaporation gas pipelines; specifically, a downstream discharge cut-off valve and a downstream discharge regulating valve are opened, the gas in the pipe with relatively high temperature after the stop of the transmission is quickly discharged to a low-pressure emptying system of a flash gas treatment plant, the gas is stopped when the second pressure transmitter indicates that the pressure is less than 0.1MPag, and at the moment, the media with the dew point pressure higher than 0.1MPag under the operating temperature in the flash gas pipeline stop of the transmission are basically discharged. If the whole flash evaporation gas treatment plant stops running, the condition that reverse purge gas is led out from the compressor and the air cooler outlet of the flash evaporation gas treatment plant is not provided any more, so that only the three steps are selected, and therefore, in the restarting process, the air inlet speed is strictly controlled, and the phenomenon that a large amount of gas instantly enters and pushes out excessive residual liquid in a pipeline to influence facilities such as a production separator of a downstream flash evaporation gas treatment plant is avoided.
Step four: after the third step is finished, starting the high-temperature gas reverse purging system and the upstream auxiliary pressure relief system; specifically, opening a reverse purging pipeline outlet block valve, establishing a balance pressure between a reverse purging pipeline and a flash gas main line (stopping transmission), opening a reverse purging pipeline inlet block valve (two paths), controlling the opening degree of a gas phase outlet regulating valve, monitoring the temperature of a temperature transmitter, controlling the mixing temperature not to exceed the maximum design temperature of the flash gas pipeline by regulating the mixing amount of flash gas with different temperatures, and controlling the flow rate of reverse purging gas not to exceed 5m/s in the flash gas pipeline; meanwhile, an inlet cut-off valve and a regulating valve of the upstream auxiliary pressure relief system are opened, and the pressure of the flash evaporation gas pipeline in the reverse purging process is kept to be not lower than 0.1 MPag. Therefore, a branch pipeline at the outlet of the compressor, a reverse purging pipeline, a main pipeline for stopping transportation and a medium reverse flow channel of an upstream emptying system are established, a three-level pressure gradient is formed, the pressure of a second pressure gradient (flash gas pipeline) is controlled to be 0.1-0.3 MPag, the distribution of residual liquid phase in the pipeline can be transferred to the front section of the pipeline under the disturbance of reverse purging gas, and enough space for receiving accumulated liquid at the upstream section in the downstream section of the pipeline can be provided for subsequent restarting operation; further, the high-temperature gas is introduced, so that the residual liquid phase medium in the pipeline is further heated and gasified and is discharged for the second time, the residual liquid phase volume in the pipeline is reduced to the maximum extent, and the liquid content of the residual gas phase is reduced by utilizing the replacement of reverse purge gas.
Step five: before restarting, starting the reverse purging system in the fourth step, closing the upstream auxiliary pressure relief system, and utilizing the reverse purging gas to realize back pressure establishment before restarting the flash evaporation gas pipeline, so that large condensate precipitation is avoided after an upstream medium (with a higher dew point) is introduced into the low-temperature pipeline.
The invention is not limited to the specific embodiments described above, but extends to any novel feature or any novel combination of features disclosed herein, or to any novel method or process steps or any novel combination of steps disclosed herein.
Claims (6)
1. The utility model provides an oil field low pressure flash distillation gas pipeline defeated hydrops control system that stops which characterized in that: the system comprises a high-temperature gas reverse purging system, an upstream auxiliary pressure relief system, a flash evaporation gas treatment plant rapid relief system and a matched detection system;
the high-temperature gas reverse purging system is connected with the flash evaporation gas main line which stops conveying, and is used for providing high-temperature gas for the flash evaporation gas main line which stops conveying, gasifying accumulated liquid in the pipeline and replacing media in the pipeline;
the upstream auxiliary pressure relief system is arranged in an upstream oil field treatment or degassing station plant and is used for flash evaporation gas relief in the process of reverse purging of a flash evaporation gas pipeline after the transportation is stopped;
the rapid discharge system of the flash evaporation gas treatment plant is arranged at the tail end of the flash evaporation gas collecting and conveying pipeline, is connected with the flash evaporation gas collecting and conveying pipeline with liquid accumulation risk and a discharge system of the flash evaporation gas treatment plant, and is used for rapidly discharging media in the flash evaporation gas pipeline after the transportation is stopped or directly discharging the flash evaporation gas pipeline when reverse purge gas is not supplied to the treatment plant;
the associated sensing system is used for sensing temperature, pressure and flow at desired locations in the system to provide operational input signals and input parameters.
2. The oilfield low pressure flash gas pipeline fluid loss control system according to claim 1, wherein: the high-temperature gas reverse purging system comprises a primary compressor outlet branch pipeline (11), a primary air cooler outlet branch pipeline (12) and a reverse purging gas mixing pipeline (13);
the outlet branch pipeline (11) of the primary compressor is connected to the outlet of a primary pressurizing unit (6) of the flash evaporation gas treatment plant and used for providing a high-temperature raw material gas after primary pressurization as a high-temperature gas source for reversely purging by a single stopping pipeline;
the primary air cooler outlet branch pipeline (12) is connected to the outlet of the air cooler (7) of the flash evaporation gas treatment plant, is used for extracting air-cooled raw material gas and is mixed with high-temperature raw material gas from the primary compressor outlet branch pipeline (11);
and the reverse purge gas mixing pipeline (13) is connected with the first-stage compressor outlet branch pipeline (11) and the first-stage air cooler outlet branch pipeline (12) and is used for conveying the mixed medium to the tail end of the flash evaporation gas gathering and conveying pipeline.
3. The oilfield low pressure flash gas pipeline fluid loss control system of claim 2, wherein: a reverse purge gas pipeline first cut-off valve (14) and a reverse purge gas pipeline first regulating valve (16) are arranged on the primary compressor outlet branch pipeline (11), and the reverse purge gas pipeline first regulating valve (16) is arranged at the downstream of the reverse purge gas pipeline first cut-off valve (14);
a second cut-off valve (15) of a reverse purge gas pipeline and a second regulating valve (17) of the reverse purge gas pipeline are arranged on the branch pipeline (12) at the outlet of the primary air cooler, and the second regulating valve (17) of the reverse purge gas pipeline is arranged at the downstream of the second cut-off valve (15) of the reverse purge gas pipeline;
and a third reverse purge gas pipeline cutoff valve (18) is arranged at the tail end of the reverse purge gas mixing pipeline (13), and is opened when the reverse purge system is started, wherein the opening sequence of the third reverse purge gas pipeline cutoff valve is prior to the first reverse purge gas pipeline cutoff valve (14) and the second reverse purge gas pipeline cutoff valve (15).
4. The oilfield low pressure flash gas pipeline fluid loss control system according to claim 1, wherein: the upstream auxiliary pressure relief system comprises an upstream relief pipeline (23), and an upstream relief pipeline cut-off valve (21) and an upstream relief regulating valve (22) which are arranged on the upstream relief pipeline (23), wherein the upstream relief pipeline cut-off valve (21) is used for providing a vent channel when a medium in a flash gas pipeline is released to a vent system of an upstream oil field treatment plant, the upstream relief regulating valve (22) is used for controlling a relief amount when the medium is released, and the upstream relief pipeline (23) is connected with the vent system built in the oil field treatment plant.
5. The oilfield low pressure flash gas pipeline fluid loss control system according to claim 1, wherein: the quick discharge system of the flash gas treatment plant comprises a flash gas pipeline downstream discharge pipeline (33), a downstream discharge cut-off valve (31) and a downstream discharge regulating valve (32), wherein the downstream discharge cut-off valve (31) and the downstream discharge regulating valve (32) are arranged on the flash gas pipeline downstream discharge pipeline (33), the downstream discharge cut-off valve (31) is opened in advance after the flash gas pipeline stops conveying, gas is accumulated in a discharge pipe, the downstream discharge regulating valve (32) and the downstream discharge cut-off valve (31) are opened simultaneously, and the flash gas pipeline downstream discharge pipeline (33) is connected with a discharge system of the flash gas treatment plant.
6. The oilfield low pressure flash gas pipeline fluid loss control system of claim 2, wherein: the matched detection system comprises a first pressure transmitter (41), a first temperature transmitter (42), a first flow transmitter (43), a second pressure transmitter (44), a second temperature transmitter (45) and a second flow transmitter (46);
the first pressure transmitter (41), the first temperature transmitter (42) and the first flow transmitter (43) are arranged at the beginning end of the reverse purge gas mixing pipeline (13) and are respectively used for detecting the pressure, the temperature and the flow of the mixed gas;
the second pressure transmitter (44) is installed at the head end of the rapid release system of the flash evaporation gas treatment plant and is used for detecting the pressure of the flash evaporation gas trunk line in real time;
the second temperature transmitter (45) and the second flow transmitter (46) are respectively installed on a discharge pipeline of the upstream auxiliary pressure discharge system and are respectively used for detecting the local medium temperature of the flash evaporation gas pipeline and the accumulated discharge medium in the flash evaporation gas reverse purging process.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022454737.4U CN213576815U (en) | 2020-10-29 | 2020-10-29 | Oil field low pressure flash distillation gas pipeline defeated hydrops control system that stops |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022454737.4U CN213576815U (en) | 2020-10-29 | 2020-10-29 | Oil field low pressure flash distillation gas pipeline defeated hydrops control system that stops |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN213576815U true CN213576815U (en) | 2021-06-29 |
Family
ID=76531279
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202022454737.4U Active CN213576815U (en) | 2020-10-29 | 2020-10-29 | Oil field low pressure flash distillation gas pipeline defeated hydrops control system that stops |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN213576815U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112178457A (en) * | 2020-10-29 | 2021-01-05 | 中国石油天然气集团有限公司 | System and method for controlling liquid conveying stoppage of low-pressure flash gas pipeline in oil field |
-
2020
- 2020-10-29 CN CN202022454737.4U patent/CN213576815U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112178457A (en) * | 2020-10-29 | 2021-01-05 | 中国石油天然气集团有限公司 | System and method for controlling liquid conveying stoppage of low-pressure flash gas pipeline in oil field |
| CN112178457B (en) * | 2020-10-29 | 2024-06-11 | 中国石油天然气集团有限公司 | System and method for controlling stop-transfusion accumulated liquid of low-pressure flash steam pipeline of oil field |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US6085546A (en) | Method and apparatus for the partial conversion of natural gas to liquid natural gas | |
| CN102099552A (en) | Method and device for operating a steam power station comprising a steam turbine and a process steam consumer | |
| CN109357163B (en) | System and method for stopping and restarting gaseous ethane pipeline | |
| CN108913252B (en) | Hydrocarbon injection dewaxing device and process suitable for dehydrating and dealkylating wax-containing natural gas | |
| CN106838605B (en) | A kind of process and device for LNG receiving stations BOG systems | |
| CN111878708A (en) | Dense-phase carbon dioxide pipeline safety discharge system and method | |
| CN213576815U (en) | Oil field low pressure flash distillation gas pipeline defeated hydrops control system that stops | |
| CN202012731U (en) | Device for recovering LNG (liquefied natural gas) evaporated gas and liquefying again | |
| CN111536420A (en) | Safe filling system and method after liquid ethane pipeline maintenance | |
| CN212273703U (en) | Dense-phase carbon dioxide pipeline safety discharge system | |
| CN111059471B (en) | Liquid ethane pipeline valve chamber relief system and method | |
| CN112178457A (en) | System and method for controlling liquid conveying stoppage of low-pressure flash gas pipeline in oil field | |
| CN208222078U (en) | Desuperheating and decompressing device for steam | |
| WO2023038650A1 (en) | System and method for harnessing energy from a pressurized gas flow to produce lng | |
| CN112524487B (en) | System and method for controlling accumulated liquid of large-caliber flash vapor pipeline of oil field | |
| CN214405626U (en) | Oil field heavy-calibre flash distillation gas pipeline hydrops control system | |
| CN108431184A (en) | The method for preparing natural gas at gas decompression station to produce liquid natural gas (LNG) | |
| CN206131510U (en) | A ejector that is used for normal atmospheric temperature natural gas to draw penetrating liquefied natural gas low temperature evaporation gas | |
| CN211344795U (en) | Liquid ethane pipeline valve chamber relief system | |
| CN114437845B (en) | Computer control method for natural gas solvent absorption denitrification process | |
| CN115342303B (en) | Efficient conveying system and method for supercritical ethane pipeline | |
| CN203144363U (en) | System for recycling gas below standard in LNG (liquefied natural gas) production | |
| CN211526879U (en) | Air separation system for semi-continuous medium-pressure nitrogen supply | |
| CN208918522U (en) | A kind of slug flow trapping system based on low pressure receiver | |
| CN206129525U (en) | Interior thermal cycle of compressor is wax deposition system not |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |